Gas-Cair, 50CDATA PERCOBAANDATA HASIL PERHITUNGAN

Lo6mmPA10.8030961387atmT50CP*A10.3026224845atmPT2.6537887298atmt (menit)Lo (mm)L (mm)L (mm)L^2 - Lo^2PB11.850692591atm06.06.00.00.0PB22.6537887298atm36.07.51.520.3PMB2.2281711723atm67.58.00.528.0DAB0.0610943574cm^2/s98.08.20.231.2DAB Lit0.4530938357cm^2/s128.28.40.234.6Kesalahan Lit86.5161799635%158.48.70.339.7188.78.80.141.4218.88.90.143.2248.99.60.756.2279.610.00.464.03010.010.30.370.1KARAKTERISTIK ASETON DAN UDARASenyawaBerat Molekul, g/molMassa Jenis, g/cm^3Titik Didih, 1 atm, Cv, cm^2/sAseton58.080.79110066.86Udara290.001294356.520.11PERHITUNGAN TEKANAN UAPPersamaan AntoineKonstanta AsetonPerry's Chemical HandbookABCKeterangan7.23161277.03237.23PTorrSuhuTCT50C323.15KPA1610.3530654228Torr0.8030961387atm2PERHITUNGAN TEKANAN UAP ASETON STANDARPersamaan AntoineKonstanta AsetonPerry's Chemical HandbookABCKeterangan7.23161277.03237.23PTorrSuhuTCT25C298.15KP*A1229.9930882133Torr0.3026224845atm3PERHITUNGAN TEKANAN TOTALTekananP1atmPT2.6537887298atm4PERHITUNGAN PB1 & PB2PB11.850692591atmPB22.6537887298atm5PERHITUNGAN PBMPBM2.22817117236PERHITUNGAN KOEFISIEN DIFUSI GASR82.06cm^3 atm/mol Km1.9417mm^2/menit0.019417cm^2/menitDAB366.5661443768mm^2/menit0.0610943574cm^2/s7PERHITUNGAN DAB LITERATURDAB Lit0.4530938357cm^2/s8PERHITUNGAN KESALAHAN LITERATURKesalahan Lit86.5161799635%

Gas-Cair, 60CDATA PERCOBAANDATA HASIL PERHITUNGAN

Lo12.5mmT60CPA11.1333115247atmP*A10.3026224845atmt (menit)Lo (mm)L (mm)L (mm)L^2 - Lo^2PT3.7449680138atm012.512.50.00.0PB12.6116564891atm312.516.84.3126.0PB23.7449680138atm616.820.33.5255.8PMB3.1443459217atm920.38.0-12.3-92.25DAB0.9928099475cm^2/s128.013.05.012.8DAB Lit0.3386638075cm^2/s1513.017.44.4146.5Kesalahan Lit193.1550185197%1817.421.94.5323.42121.927.35.4589.02427.331.84.5855.02731.835.84.01125.43035.838.93.11357.0KARAKTERISTIK ASETON DAN UDARASenyawaBerat Molekul, g/molMassa Jenis, g/cm^3Titik Didih, 1 atm, Cv, cm^2/sAseton58.080.79110066.86Udara290.001294356.520.11PERHITUNGAN TEKANAN UAPPersamaan AntoineKonstanta AsetonPerry's Chemical HandbookABCKeterangan7.23161277.03237.23PTorrSuhuTCT60C333.15KPA1861.3167587461Torr1.1333115247atm2PERHITUNGAN TEKANAN UAP ASETON STANDARPersamaan AntoineKonstanta AsetonPerry's Chemical HandbookABCKeterangan7.23161277.03237.23PTorrSuhuTCT25C298.15KP*A1229.9930882133Torr0.3026224845atm3PERHITUNGAN TEKANAN TOTALTekananP1atmPT3.7449680138atm4PERHITUNGAN PB1 & PB2PB12.6116564891atmPB23.7449680138atm5PERHITUNGAN PBMPBM3.14434592176PERHITUNGAN KOEFISIEN DIFUSI GASR82.06cm^3 atm/mol Km43.191mm^2/menit0.43191cm^2/menitDAB5956.859685082mm^2/menit0.9928099475cm^2/s7PERHITUNGAN DAB LITERATURDAB Lit0.3386638075cm^2/s8PERHITUNGAN KESALAHAN LITERATURKesalahan Lit193.1550185197%

Cair-Cair, 1MDATA PERCOBAANKCl1M0.001mol/cm^3t (menit)Konduktivitas (miu S)Konduktivitas (S)06.10.0000061037.60.0000076067.80.0000078098.00.00000800128.10.00000810158.30.00000830188.40.00000840218.50.00000850248.50.00000850278.50.00000850308.50.00000850Data PeralatanN121buahD0.1cmL0.5cmV tangki900cm^3CM0.41mol/cm^31PERHITUNGAN KOEFISIEN DIFUSI GASm0.00000006dK/dt0.00000006S/detikDAB0.0693305875cm^2/detik2PERHITUNGAN DAB LITERATUR2.65Mb18gr/molT298.15CViskositas air0.01gr/cm detikDAB Lit0.9614478286cm^2/detik3PERHITUNGAN KESALAHAN LITERATURKesalahan Lit92.788939198%

Cair-Cair, 2MDATA PERCOBAANKCl2M0.002mol/cm^3t (menit)Konduktivitas (miu S)Konduktivitas (S)063.30.0000633365.60.0000656666.10.0000661966.40.00006641267.10.00006711567.20.00006721867.30.00006732167.60.00006762467.80.000067827680.00006803068.20.0000682Data PeralatanN121buahD0.1cmL0.5cmV tangki900cm^3CM0.41mol/cm^31PERHITUNGAN KOEFISIEN DIFUSI GASm0.0000007dK/dt0.0000007S/detikDAB0.4044284271cm^2/detik2PERHITUNGAN DAB LITERATUR2.65Mb18gr/molT298.15CViskositas air0.01gr/cm detikDAB Lit0.6343190078cm^2/detik3PERHITUNGAN KESALAHAN LITERATURKesalahan Lit36.2421081354%